2015
DOI: 10.1149/2.0871504jes
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Electrochemical Preparation of Fine Powders of Nickel-Boron Alloys in Molten Chlorides for Magnetic Hydrogenation Catalysts

Abstract: Fine powders of magnetic nickel-boron alloys were prepared for the first time by direct electrochemical reduction of the 2Ni 3 (BO 3 ) 2 /B 2 O 3 , Ni 3 (BO 3 ) 2 /NiO and Ni 3 (BO 3 ) 2 /3NiO composite precursors in molten CaCl 2 -NaCl at 700• C. Precursors with different nickel to boron atomic ratios (R Ni/B = 1, 2 or 3) were synthesized by the sol-gel process followed by thermal annealing at 750• C. The reduction pathway, phase transformation and morphology of the samples electrolyzed at different voltages … Show more

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Cited by 7 publications
(2 citation statements)
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“…Since the FFC-Cambridge process uses the electric current to remove the oxygen from the cathode, the current efficiency can be estimated from the following relation: assuming the weight losses is due to the removal of oxygen from the pellets, the current efficiency can be calculated according to the measured mass loss of the pellets and the mass loss, due to removal of oxygen, calculated from the total electrolysis charge. 22 Hence, the obtained current efficiency is 50% and the energy consumption for the production of Cr 1.12 Ni 2.88 is about 6.66 kW h/kg. The current efficiency could be even higher if the As the phase changes with the electrolysis progresses, the morphologies of the particles in the pellet change dramatically and nodular particles of porous structure observed to be sintered lightly are synthesized after 4 h electro-reduction.…”
Section: Electro-reduction Pathways and Microstructural Changes-inmentioning
confidence: 90%
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“…Since the FFC-Cambridge process uses the electric current to remove the oxygen from the cathode, the current efficiency can be estimated from the following relation: assuming the weight losses is due to the removal of oxygen from the pellets, the current efficiency can be calculated according to the measured mass loss of the pellets and the mass loss, due to removal of oxygen, calculated from the total electrolysis charge. 22 Hence, the obtained current efficiency is 50% and the energy consumption for the production of Cr 1.12 Ni 2.88 is about 6.66 kW h/kg. The current efficiency could be even higher if the As the phase changes with the electrolysis progresses, the morphologies of the particles in the pellet change dramatically and nodular particles of porous structure observed to be sintered lightly are synthesized after 4 h electro-reduction.…”
Section: Electro-reduction Pathways and Microstructural Changes-inmentioning
confidence: 90%
“…[4][5][6] This process has critical shortcomings such as its being hard to produce a homogeneous alloy composition as a result of the large melting point (Ni, 1453 • C; Cr, 1875 • C), density (Ni, 8.9 g/cm 3 ; Cr, 7.19 g/cm 3 ) difference and a complicated production process that requires significant amounts of energy and cost. [4][5][6] The recent electrochemical reduction, namely the FFC-Cambridge process, of pure or mixed oxide powder to metal or alloy in molten salt offers an alternative technology for the metallurgical industry, and so far has been demonstrated for successful production of transition metal and alloy including Ti, [7][8][9] Cr, [10][11][12][13][14][15] Ta, 16 Cr 7 C 3 , 17 La 2 (Ni 1-x Co x ) 7 (x = 0.05, 0.1, 0.2), 18 Ni-Nd, 19 Co-Cr, 20 Fe-Ti, 21 and nickel-boron, 22 et al O 2− is released from the solid oxide cathode and diffuses toward the graphite anode through the molten salt, which discharges at the graphite anode and liberates as CO or CO 2 under the influence of the applied voltage and the high temperature of the molten salt. 23 This method is a much easier, less expensive and more environmentally friendly process.…”
mentioning
confidence: 99%